Catalyst components for polymerization of olefins

ABSTRACT

A process for the polymerization of olefinic hydrocarbons is carried out in the presence of a catalyst comprising a catalyst component derived from reacting a compound of the formula Me 1  R 1   n  X 1   4-n , a compound of the formula Me 2  R 2   m  X 2   z-m , an organocyclic compound having two or more conjugated double bonds and a carrier of inorganic or polymeric material, and a modified organoaluminum compound having Al--O--Al bonds, the resulting polyolefins having a relatively wide molecular weight distribution, a relatively narrow composition distribution and increased bulk density.

This is a continuation of application Ser. No. 08/212,449, filed Mar.14, 1994, now abandoned, which is a continuation of application Ser. No.07/974,546, filed Nov. 12, 1992, now U.S. Pat. No. 5,331,071.

BACKGROUND OF THE INVENTION

1. Field of the Invention

This invention relates to a process for the manufacture of olefinicpolymers in the presence of a selected catalyst.

2. Prior Art

Catalyst compositions comprising zirconium compounds, typicallymetallocene and aluminoxane are known for use in the homopolymerizationof olefins such as ethylene or the copolymerization ofethylene/alpha-olefins as disclosed for example in Japanese Laid-OpenPatent Publication No. 58-19309. While the disclosed prior art processis advantageous so far as concerns the availability of polymerizedproducts at increased rate of yield, it has a drawback in that thepolymers obtained have a relatively narrow distribution of molecularweight or composition, coupled with a relatively low molecular weight.When taking into account the molecular weight alone, it would bepossible to increase the molecular weight of a polymer to some extent bymaking a proper selection of transition metals from among the group ofmetallocene. The molecular weight of a polymer may be increased by theuse of a transition metal compound having a 2,3 and 4-substitutedcyclopentadienyl group as disclosed in Japanese Laid-Open PatentPublication No. 63-234005, or by the use of a hafnium compound having aligand bonded to at least two cross-linked conjugated cycloalkadienylgroups as disclosed in Japanese Laid-Open Patent Publication No.2-22307. However, such catalyst components are complicated if notdifficult to synthesize. The use of hafnium compounds is not veryconducive to polymer yields. The prior catalysts being often soluble inthe reaction system are further disadvantageous in that the polymerresulting from slurry or gas-phase polymerization would have reducedbulk density and deteriorated granular properties.

SUMMARY OF THE INVENTION

With the foregoing difficulties of the prior art in view, the presentinvention seeks to provide a process for the manufacture of polyolefinsin the presence of a novel catalyst at increased rate of yields, whichpolyolefins have a relatively wide molecular weight distribution, anarrow composition distribution and improved granular quality.

This and other objects and features of the invention will appear clearfrom the following detailed description of certain preferredembodiments.

According to the invention, there is provided a process for themanufacture of polyolefins which comprises polymerizing a wide range ofolefinic hydrocarbons in the presence of a catalyst composition whichcomprises a first component (I) and a second component (II), saidcomponent (I) resulting from the reaction of a compound (i) of theformula

    Me.sup.1 R.sup.1.sub.n X.sup.1.sub.4-n

wherein R¹ is a hydrocarbon moiety of 1-24 carbon atoms, X¹ is a halogenatom, Me¹ is a metal of the group of zirconium, titanium and hafnium,and n is an integer of 0≦n≦4;

a compound (ii) of the formula

    Me.sup.2 R.sup.2.sub.m X.sup.2.sub.z-m

wherein R² is a hydrocarbon group of 1-24 carbon atoms, X² is an alkoxygroup of 1-12 carbon atoms or a halogen atom, Me² is an element of I-IIIGroups in the Periodic Table, z is the valence of Me², and m is aninteger of 0≦m≦3; an organocyclic compound (iii) having two or moreconjugated double bonds; and an inorganic carrier and/or particulatepolymer carrier (iv), said component (II) being a modifiedorganoaluminum compound having Al--O--Al bonds derived from the reactionof an organoaluminum compound and water.

BRIEF DESCRIPTION OF THE DRAWING

FIG. 1 is a flow chart utilized to explain the process of preparing acatalyst used in the invention.

DETAILED DESCRIPTION OF THE INVENTION

The compound (i) which is used in the preparation of Component (I) ofthe inventive catalyst composition is represented by the formula Me¹ R¹_(n) X¹ _(4-n) wherein R¹ is a hydrocarbon moiety having a carbon numberof from 1 to 24, preferably from 1 to 8, including an alkyl group suchas methyl, ethyl, propyl, butyl, pentyl, hexyl and octyl an alkenylgroup such as vinyl and allyl, an aryl group such as phenyl, tolyl andxylyl, an aralkyl group such as benzyl, phenethyl, styryl and neophyl*,an alkoxy group such as methoxy, ethoxy, propoxy, butoxy and pentyloxy,an aryloxy group such as phenoxy and tolyoxy, and an aralkyloxy groupsuch as benzyloxy. X¹ in the formula is a halogen atom such as fluorine,iodine, chlorine and bromine. Me¹ is titanium, zirconium or hafnium,ziconium being preferred. n is 0≦n≦4, preferably 0≦n≦4.

Specific examples of the compound (i) include tetramethyl zirconium,tetraethyl zirconium, tetrapropyl zirconium, tetra-n-butyl zirconium,tetrapentyl zirconium, tetraphenyl zirconium, tetratolyl zirconium,tetrabenzyl zirconium, tetramethoxy zirconium, tetraethoxy zirconium,tetrapropoxy zirconium, tetrabutoxy zirconium, tetraphenoxy zirconium,tetratolyoxy zirconium, tetrapentyloxy zirconium, tetrabenzyloxyzirconium, tetraallyl zirconium, tetraneophyl zirconium,trimethylmonochlorozirconium, triethylmonochlorozirconium,tripropylmonochlorozirconium, tri-n-butylmonochlorozirconium,tribenzylmonochlorozirconium, dimethyldichlorozirconium,diethyldichlorozirconium, di-n-butyldichlorozirconium,dibenzyldichlorozirconium, monomethyltrichlorozirconium,monoethyltrichlorozirconium, mono-n-butyltrichlorozirconium,monobenzyltrichlorozirconium, tetrachlorozirconium,tetramethoxyzirconium, trimethoxymonochlorozirconium,dimethoxydichlorozirconium, monomethoxytrichlorozirconium,tetraethoxyzirconium, triethoxymonochlorozirconium,diethoxydichlorozirconium, monoethoxytrichlorozirconium,tetraisopropoxyzirconium, triisopropoxymonochlorozirconium,diisopropoxydichlorozirconium, monoisopropoxytrichlorozirconium,tetra-n-butoxyzirconium, tri-n-butoxymonochlorozirconium,di-n-butoxydichlorozirconium, mono-n-butoxytrichlorozirconium,tetrapentoxyzirconium, tripentoxymonochlorozirconium,dipentoxydichlorozirconium, monopentoxytrichlorozirconium,tetraphenoxyzirconium, triphenoxymonochlorozirconium,diphenoxydichlorozirconium, monophenoxytrichlorozirconium,tetratolyoxyzirconium, tritolyoxymonochlorozirconium,ditolyoxydichlorozirconium, monotolyoxytrichlorozirconium,tetrabenzyloxyzirconium, tribenzyloxymonochlorozirconium,dibenzyloxydichlorozirconium, monobenzyloxytrichlorozirconium,trimethylmonobromozirconium, triethylmonobromozirconium,tripropylmonobromozirconium, tri-n-butylmonobromozirconium,tribenzylmonobromozirconium, dimethyldibromozirconium,diethyldibromozirconium, di-n-butyldibromozirconium,dibenzyldibromozirconium, monomethyltribromozirconium,monoethyltribromozirconium, mono-n-butyltribromozirconium,monobenzyltribromozirconium, tetrobromozirconium,trimethoxymonobromozirconium, dimethoxydibromozirconium,monomethoxytribromozirconium, triethoxymonobromozirconium,diethoxydibromozirconium, monoethoxytribromozirconium,triisopropoxymonobromozirconium, diisopropoxydibromozirconium,monoisopropoxytribromozirconium, tri-n-butoxymonobromozirconium,di-n-butoxydibromozirconium, mono-n-butoxytribromozirconium,tripentoxymonobromozirconium, dipentoxydibromozirconium,monopentoxytribromozirconium, triphenoxymonobromozirconium,diphenoxydibromozirconium, monophenoxytribromozirconium,tritolyloxymonobromozirconium, ditolyloxydibromozirconium,monotolyloxytribromozirconium, tribenzloxymonobromozirconium,dibenzloxydibromozirconium, monobenzloxytribromozirconium,trimethylmonoiodozirconium, triethylmonoiodozirconium,tripropylmonoiodozirconium, tri-n-butylmonoiodozirconium,tribenzylmonoiodozirconium, dimethyldiioxozirconium,diethyldiioxozirconium, dipropyldiioxozirconium,di-n-butyldiioxozirconium, dibenzyldiioxozirconium,monomethyltriiodozirconium, monoethyltriiodozirconium,monopropyltriiodozirconium, mono-n-butyltriiodozirconium,monobenzyltriiodozirconium, tetraiodozirconium,trimethoxymonoiodozirconium, dimethoxydiiodozirconium,monomethoxytriiodozirconium, triethoxymonoiodozirconium,diethoxydiiodozirconium, monoethoxytriiodozirconium,triisopropoxymonoiodozirconium, diisopropoxydiiodozirconium,monoisopropoxytriiodozirconium, tri-n-butoxymonoiodozirconium,di-n-butoxydiiodozirconium, mono-n-butoxytriiodozirconium,tripentoxymonoiodozirconium, dipentoxydiiodozirconium,monopentoxytriiodozirconium, triphenoxymonoiodozirconium,diphenoxydiiodozirconium, monophenoxytriiodozirconium,tritolyoxymonoiodoiodozirconium, ditolyoxydiiodozirconium,monotolyoxytriiodozirconium, tribenzyloxymonoiodozirconium,dibenzyloxydiiodozirconium, monobenzyloxytriiodozirconium,tribenzylmonomethoxyzirconium, tribenzylmonoethoxyzirconium,tribenzylmonopropoxyzirconium, tribenzylmonobutoxyzirconium,tribenzylmonophenoxyzirconium, dibenzyldimethoxyzirconium,dibenzyldiethoxyzirconium, dibenzyldipropoxyzirconium,dibenzyldibutoxyzirconium, dibenzyldiphenoxyzirconium,monobenzyltrimethoxyzirconium, monobenzyltriethoxyzirconium,monobenzyltripropoxyzirconium, monobenzyltributoxyzirconium,monobenzyltriphenoxyzirconium, trineophylmonomethoxyzirconium,trineophylmonoethoxyzirconium, trineophylmonopropoxyzirconium,trineophylmonobutoxyzirconium, trineophylmonophenoxyzirconium,dineophyldimethoxyzirconium, dineophyldiethoxyzirconium,dineophyldipropoxyzirconium, dineophyldibutoxyzirconium,dineophyldiphenoxyzirconium, mononeophyltrimethoxyzirconium,mononeophyltriethoxyzirconium, mononeophyltripropoxyzirconium,mononeophyltributoxyzirconium, mononeophyltriphenoxyzirconium,tetramethyl titanium, tetraethyl titanium, tetrapropyl titanium,tetra-n-butyl titanium, tetrapentyl titanium, tetraphenyl titanium,tetraatolyl titanium, tetrabenzyl titanium, tetramethoxy titanium,tetraethoxy titanium, tetrapropoxy titanium, tetrabutoxy titanium,tetraphenoxy titanium, tetratolyoxy titanium, tetrapentyloxy titanium,tetrabenzyloxy titanium, tetraallyl titanium, tetraneophyl titanium,trimethylmonochlorotitanium, triethylmonochlorotitanium,tripropylmonochlorotitanium, tri-n-butylmonochlorotitanium,tribenzylmonochlorotitanium, dimethyldichlorotitanium,diethyldichlorotitanium, di-n-butyldichlorotitanium,dibenzyldichlorotitanium, monomethyltrichlorotitanium,monoethyltrichlorotitanium, mono-n-butyltrichlorotitanium,monobenzyltrichlorotitanium, tetrachlorotitanium, tetramethoxytitanium,trimethoxymonochlorotitanium, dimethoxydichlorotitanium,monomethoxytrichlorotitanium, tetraethoxytitanium,triethoxymonochlorotitanium, diethoxydichlorotitanium,monoethoxytrichlorotitanium, tetraisopropoxytitanium,triisopropoxymonochlorotitanium, diisopropoxydichlorotitanium,monoisopropoxytrichlorotitanium, tetra-n-butoxytitanium,tri-n-butoxymonochlorotitanium, di-n-butoxydichlorotitanium,mono-n-butoxytrichlorotitanium, tetrapentoxytitanium,tripentoxymonochlorotitanium, dipentoxydichlorotitanium,monopentoxytrichlorotitanium, tetraphenoxytitanium,triphenoxymonochlorotitanium, diphenoxydichlorotitanium,monophenoxytrichlorotitanium, tetratolyoxytitanium,tritolyoxymonochlorotitanium, ditolyoxydichlorotitanium,monotolyoxytrichlorotitanium, tetrabenzyloxytitanium,tribenzyloxymonochlorotitanium, dibenzyloxydichlorotitanium,monobenzyloxytrichlorotitanium, trimethylmonobromotitanium,triethylmonobromotitanium, tripropylmonobromotitanium,tri-n-butylmonobromotitanium, tribenzylmonobromotitanium,dimethyldibromotitanium, diethyldibromotitanium,di-n-butyldibromotitanium, dibenzyldibromotitanium,monomethyltribromotitanium, monoethyltribromotitanium,mono-n-butyltribromotitanium, monobenzyltribromotitanium,tetrobromotitanium, trimethoxymonobromotitanium,dimethoxydibromotitanium, monomethoxytribromotitanium,triethoxymonobromotitanium, diethoxydibromotitanium,monoethoxytribromotitanium, triisopropoxymonobromotitanium,diisopropoxydibromotitanium, monoisopropoxytribromotitanium,tri-n-butoxymonobromotitanium, di-n-butoxydibromotitanium,mono-n-butoxytribromotitanium, tripentoxymonobromotitanium,dipentoxydibromotitanium, monopentoxytribromotitanium,triphenoxymonobromotitanium, diphenoxydibromotitanium,monophenoxytribromotitanium, tritolyloxymonobromotitanium,ditolyloxydibromotitanium, monotolyloxytribromotitanium,tribenzloxymonobromotitanium, dibenzloxydibromotitanium,monobenzloxytribromotitanium, trimethylmonoiodotitanium,triethylmonoiodotitanium, tripropylmonoiodotitanium,tri-n-butylmonoiodotitanium, tribenzylmonoiodotitanium,dimethyldiioxotitanium, diethyldiioxotitanium, dipropyldiioxotitanium,di-n-butyldiioxotitanium, dibenzyldiioxotitanium,monomethyltriiodotitanium, monoethyltriiodotitanium,monopropyltriiodotitanium, mono-n-butyltriiodotitanium,monobenzyltriiodotitanium, tetraiodotitanium,trimethoxymonoiodotitanium, dimethoxydiiodotitanium,monomethoxytriiodotitanium, triethoxymonoiodotitanium,diethoxydiiodotitanium, monoethoxytriiodotitanium,triisopropoxymonoiodotitanium, diisopropoxydiiodotitanium,monoisopropoxytriiodotitanium, tri-n-butoxymonoiodotitanium,di-n-butoxydiiodotitanium, mono-n-butoxytriiodotitanium,tripentoxymonoiodotitanium, dipentoxydiiodotitanium,monopentoxytriiodotitanium, triphenoxymonoiodotitanium,diphenoxydiiodotitanium, monophenoxytriiodotitanium,tritolyoxymonoiodoiodotitanium, ditolyoxydiiodotitanium,monotolyoxytriiodotitanium, tribenzyloxymonoiodotitanium,dibenzyloxydiiodotitanium, monobenzyloxytriiodotitanium,tribenzylmonomethoxytitanium, tribenzylmonoethoxytitanium,tribenzylmonopropoxytitanium, tribenzylmonobutoxytitanium,tribenzylmonophenoxytitanium, dibenzyldimethoxytitanium,dibenzyldiethoxytitanium, dibenzyldipropoxytitanium,dibenzyldibutoxytitanium, dibenzyldiphenoxytitanium,monobenzyltrimethoxytitanium, monobenzyltriethoxytitanium,monobenzyltripropoxytitanium, monobenzyltributoxytitanium,monobenzyltriphenoxytitanium, trineophylmonomethoxytitanium,trineophylmonoethoxytitanium, trineophylmonopropoxytitanium,trineophylmonobutoxytitanium, trineophylmonophenoxytitanium,dineophyldimethoxytitanium, dineophyldiethoxytitanium,dineophyldipropoxytitanium, dineophyldibutoxytitanium,dineophyldiphenoxytitanium, mononeophyltrimethoxytitanium,mononeophyltriethoxytitanium, mononeophyltripropoxytitanium,mononeophyltributoxytitanium, mononeophyltriphenoxytitanium, tetramethylhafnium, tetraethyl hafnium, tetrapropyl hafnium, tetra-n-butyl hafnium,tetrapentyl hafnium, tetraphenyl hafnium, tetraatolyl hafnium,tetrabenzyl hafnium, tetramethoxy hafnium, tetraethoxy hafnium,tetrapropoxy hafnium, tetrabutoxy hafnium, tetraphenoxy hafnium,tetratolyoxy hafnium, tetrapentyloxy hafnium, tetrabenzyloxy hafnium,tetraallyl hafnium, tetraneophyl hafnium, trimethylmonochlorohafnium,triethylmonochlorohafnium, tripropylmonochlorohafnium,tri-n-butylmonochlorohafnium, tribenzylmonochlorohafnium,dimethyldichlorohafnium, diethyldichlorohafnium,di-n-butyldichlorohafnium, dibenzyldichlorohafnium,monomethyltrichlorohafnium, monoethyltrichlorohafnium,mono-n-butyltrichlorohafnium, monobenzyltrichlorohafnium,tetrachlorohafnium, tetramethoxyhafnium, trimethoxymonochlorohafnium,dimethoxydichlorohafnium, monomethoxytrichlorohafnium,tetraethoxyhafnium, triethoxymonochlorohafnium, diethoxydichlorohafnium,monoethoxytrichlorohafnium, tetraisopropoxyhafnium,triisopropoxymonochlorohafnium, diisopropoxydichlorohafnium,monoisopropoxytrichlorohafnium, tetra-n-butoxyhafnium,tri-n-butoxymonochlorohafnium, di-n-butoxydichlorohafnium,mono-n-butoxytrichlorohafnium, tetrapentoxyhafnium,tripentoxymonochlorohafnium, dipentoxydichlorohafnium,monopentoxytrichlorohafnium, tetraphenoxyhafnium,triphenoxymonochlorohafnium, diphenoxydichlorohafnium,monophenoxytrichlorohafnium, tetratolyoxyhafnium,tritolyoxymonochlorohafnium, ditolyoxydichlorohafnium,monotolyoxytrichlorohafnium, tetrabenzyloxyhafnium,tribenzyloxymonochlorohafnium, dibenzyloxydichlorohafnium,monobenzyloxytrichlorohafnium, trimethylmonobromohafnium,triethylmonobromohafnium, tripropylmonobromohafnium,tri-n-butylmonobromohafnium, tribenzylmonobromohafnium,dimethyldibromohafnium, diethyldibromohafnium, di-n-butyldibromohafnium,dibenzyldibromohafnium, monomethyltribromohafnium,monoethyltribromohafnium, mono-n-butyltribromohafnium,monobenzyltribromohafnium, tetrobromohafnium,trimethoxymonobromohafnium, dimethoxydibromohafnium,monomethoxytribromohafnium, triethoxymonobromohafnium,diethoxydibromohafnium, monoethoxytribromohafnium,triisopropoxymonobromohafnium, diisopropoxydibromohafnium,monoisopropoxytribromohafnium, tri-n-butoxymonobromohafnium,di-n-butoxydibromohafnium, mono-n-butoxytribromohafnium,tripentoxymonobromohafnium, dipentoxydibromohafnium,monopentoxytribromohafnium, triphenoxymonobromohafnium,diphenoxydibromohafnium, monophenoxytribromohafnium,tritolyloxymonobromohafnium, ditolyloxydibromohafnium,monotolyloxytribromohafnium, tribenzloxymonobromohafnium,dibenzloxydibromohafnium, monobenzloxytribromohafnium,trimethylmonoiodohafnium, triethylmonoiodohafnium,tripropylmonoiodohafnium, tri-n-butylmonoiodohafnium,tribenzylmonoiodohafnium, dimethyldiioxohafnium, diethyldiioxohafnium,dipropyldiioxohafnium, di-n-butyldiioxohafnium, dibenzyldiioxohafnium,monomethyltriiodohafnium, monoethyltriiodohafnium,monopropyltriiodohafnium, mono-n-butyltriiodohafnium,monobenzyltriiodohafnium, tetraiodohafnium, trimethoxymonoiodohafnium,dimethoxydiiodohafnium, monomethoxytriiodohafnium,triethoxymonoiodohafnium, diethoxydiiodohafnium,monoethoxytriiodohafnium, triisopropoxymonoiodohafnium,diisopropoxydiiodohafnium, monoisopropoxytriiodohafnium,tri-n-butoxymonoiodohafnium, di-n-butoxydiiodohafnium,mono-n-butoxytriiodohafnium, tripentoxymonoiodohafnium,dipentoxydiiodohafnium, monopentoxytriiodohafnium,triphenoxymonoiodohafnium, diphenoxydiiodohafnium,monophenoxytriiodohafnium, tritolyoxymonoiodoiodohafnium,ditolyoxydiiodohafnium, monotolyoxytriiodohafnium,tribenzyloxymonoiodohafnium, dibenzyloxydiiodohafnium,monobenzyloxytriiodohafnium, tribenzylmonomethoxyhafnium,tribenzylmonoethoxyhafnium, tribenzylmonopropoxyhafnium,tribenzylmonobutoxyhafnium, tribenzylmonophenoxyhafnium,dibenzyldimethoxyhafnium, dibenzyldiethoxyhafnium,dibenzyldipropoxyhafnium, dibenzyldibutoxyhafnium,dibenzyldiphenoxyhafnium, monobenzyltrimethoxyhafnium,monobenzyltriethoxyhafnium, monobenzyltripropoxyhafnium,monobenzyltributoxyhafnium, monobenzyltriphenoxyhafnium,trineophylmonomethoxyhafnium, trineophylmonoethoxyhafnium,trineophylmonopropoxyhafnium, trineophylmonobutoxyhafnium,trineophylmonophenoxyhafnium, dineophyldimethoxyhafnium,dineophyldiethoxyhafnium, dineophyldipropoxyhafnium,dineophyldibutoxyhafnium, dineophyldiphenoxyhafnium,mononeophyltrimethoxyhafnium, mononeophyltriethoxyhafnium,mononeophyltripropoxyhafnium, mononeophyltributoxyhafnium,mononeophyltriphenoxyhafnium and the like, most preferred of whichcompounds are tetramethylzirconium tetraethylzirconium,tetrabenzylzirconium, tetrapropoxyzirconium, tetrabutoxyzirconium andtetrachlorozirconium.

The compound (ii) used in the invention is represented by the formulaMe² R² _(m) X² _(z-m) wherein R² is a hydrocarbon group having a carbonnumber of from 1 to 24, preferably from 1 to 12, more preferably from 1to 8, including an alkyl group such as methyl, ethyl, propyl, isopropyl,butyl, pentyl, hexyl, octyl, decyl and dodecyl, an alkenyl group such asvinyl and allyl, an aryl group such as phenyl, tolyl and xylyl, and anaralkyl group such as benzyl, phenethyl and styryl; X² is an alkoxygroup of 1-12 carbon atoms, preferably 1-6 carbon atoms such as methoxy,ethoxy, propoxy and butoxy, or a halogen atom such as fluorine, iodine,chlorine and bromine; Me² is an element of Groups I-III in the PeriodicTable; z is the valence of Me² ; and m is an integer of 0≦m≦3.

Specific examples of the compound (ii) eligible for the purpose of theinvention are methyllithium, ethyllithium, n-propyllithium,isopropyllithium, n-butyllithium, t-butyllithium, pentyllithium,octyllithium, phenyllithium, benzyllithium, dimethylmagnesium,diethylmagnesium, di-n-propylmagnesium, diisopropylmagnesium,di-n-butylmagnesium, di-t-butylmagnesium, dipentylmagnesium,methylmagnesium chloride, n-propylmagnesium chloride, isopropylmagnesiumchloride, n-butylmagnesium chloride, t-butylmagnesium chloride,pentylmagnesium chloride, octylmagnesium chloride, phenylmagnesiumchloride, benzylmagnesium chloride, methylmagnesium bromide,methylmagnesium iodide, ethylmagnesium bromide, ethylmagnesium iodide,n-propylmagnesium bromide, n-propylmagnesium iodide, isopropylmagnesiumbromide, isopropylmagnesium iodide, n-butylmagnesium bromide,n-butylmagnesium iodide, t-butylmagnesium bromide, t-butylmagnesiumiodide, pentylmagnesium bromide, pentylmagnesium iodide, octylmagnesiumbromide, octylmagnesium iodide, phenylmagnesium bromide, phenylmagnesiumiodide, benzylmagnesium bromide, benzylmagnesium iodide, dimethylzinc,diethylzinc, di-n-propylzinc, diisopropylzinc, di-n-butylzinc,di-t-butylzinc, dipentylzinc, dioctylzinc, diphenylzinc, dibenzylzinc,trimethylboron, triethylboron, tri-n-propylboron, triisopropylboron,tri-n-butylboron, tri-t-butylboron, tripentylboron, trioctylboron,triphenylboron and tribenzylboron.

The compound (ii) further includes an organoaluminum compound of theformulae R₃ Al, R₂ AlX, RAlX₂, RAl(OR)X or R₃ Al₂ X₃ wherein R is ahydrocarbon group of 1-5 carbon atoms and X is a halogen atom, specificexamples of which include trimethylaluminum, triethylaluminum,diethylaluminum chloride, diethylaluminum bromide, diethylaluminumfluoride, diethylaluminum iodide, ethylaluminum dichloride,ethylaluminum dibromide, ethylaluminum difluoride ethylaluminumdiiodide, tripropylaluminum, dipropylaluminum chloride, dipropylaluminumbromide, dipropylaluminum fluoride dipropylaluminum iodide,propylaluminum dichloride, propylaluminum dibromide, propylaluminumdifluoride propylaluminum diiodide, triisopropylaluminum,diisopropylaluminum chloride, diisopropylaluminum bromide,diisopropylaluminum fluoride, diisopropylaluminum iodide, ethylaluminumsesquichloride, ethylaluminum sesquibromide, propylaluminumsesquichloride, propylaluminum sesquibromide, n-buthylaluminumsesquichloride, n-buthylaluminum sesquibromide, isopropylaluminumdichloride, isopropylaluminum dibromide, isopropylaluminum difluoride,isopropylaluminum diiodide, tributylaluminum, dibutylaluminum chloride,dibutylaluminum bromide, dibutylaluminum fluoride, dibutylaluminumiodide, butylaluminum dichloride, butylaluminum dibromide, butylaluminumdifluoride, butylaluminum diiodide, tri-sec-butylaluminum,di-sec-butylaluminum chloride, di-sec-butylaluminum bromide,di-sec-butylaluminum fluoride, di-sec-butylaluminum iodide,sec-butylaluminum dichloride, sec-butylaluminum dibromide,sec-butylaluminum difluoride, sec-butylaluminum diiodide,tri-tert-butylaluminum, di-tert-butylaluminum chloride,di-tert-butylaluminum bromide, di-tert-butylaluminum fluoride,di-tert-butylaluminum iodide, tert-butylaluminum dichloride,tert-butylaluminum dibromide, tert-butylaluminum difluoride,tert-butylaluminum diiodide, triisobutylaluminum, diisobutylaluminumchloride, diisobutylaluminum bromide, diisobutylaluminum fluoride,diisobutylaluminum iodide, isobutylaluminum dichloride, isobutylaluminumdibromide, isobutylaluminum difluoride, isobutylaluminum diiodide,trihexylaluminum, dihexylaluminum chloride, dihexylaluminum bromide,dihexylaluminum fluoride, dihexylaluminum iodide, hexylaluminumdichloride, hexylaluminum dibromide, hexylaluminum difluoride,hexylaluminum diiodide, tripentylaluminum, dipentylaluminum chloride,dipentylaluminum bromide, dipentylaluminum fluoride, dipentylaluminumiodide, pentylaluminum dichloride, pentylaluminum dibromide,pentylaluminum difluoride, pentylaluminum diiodide, methylaluminummethoxide, methylaluminum ethoxide, methylaluminum propoxide,methylaluminum butoxide, dimethylaluminum methoxide, dimethylaluminumethoxide, dimethylaluminum propoxide, dimethylaluminum butoxide,ethylaluminum methoxide, ethylaluminum ethoxide, ethylaluminumpropoxide, ethylaluminum butoxide, diethylaluminum methoxide,diethylaluminum ethoxide, diethylaluminum propoxide, diethylaluminumbutoxide, propylaluminum methoxide, propylaluminum ethoxide,propylaluminum propoxide, propylaluminum butoxide, dipropylaluminummethoxide, dipropylaluminum ethoxide, dipropylaluminum propoxide,dipropylaluminum butoxide, butylaluminum methoxide, butylaluminumethoxide, butylaluminum propoxide, butylaluminum butoxide,dibutylaluminum ethoxide, dibutylaluminum propoxide, dibutylaluminumbutoxide and the like.

The compound (iii) is an organocyclic compound having two or moreconjugated double bonds, examples of which include a cyclic hydrocarboncompound having two or more, preferably 2-4, more preferably 2-3,conjugated double bonds and a carbon number of 4-24, preferably 4-12, inthe molecule such as an aralkylene of 7-24 carbon atoms,cyclopentadiene, substituted cyclopentadiene, indene, substitutedindene, fluorene, substituted fluorene, cycloheptatriene, substitutedcycloheptatriene, cyclooctatetraene and substituted cyclooctatetraene.Each of such substituted compounds has a substituting group such asalkyl or aralkyl of 1-12 carbon atoms.

Specific examples of the compound (iii) include cyclopentadiene,methylcyclopentadiene, ethylcyclopentadiene, t-butylcyclopentadiene,hexylcyclopentadiene, octylcyclopentadiene, 1,2-dimethylcyclopentadiene,1,3-dimethylcyclopentadiene, 1,2,4-trimethylcyclopentadiene,1,2,3,4-tetramethylcyclopentadiene, pentamethylcyclopentadiene, indene,4-methyl-1-indene, 4,7-dimethylindene, 4,5,6,7-tetrahydroindene,fluorene, methylfluorene, cycloheptatriene, methylcycloheptatriene,cyclooctatraene and methylcyclooctatraene. These compounds may be bondedthrough the medium of an alkylene group of 2-8, preferably 2-3, carbonatoms, such bonded compounds including for example bis-indenylethane,bis(4,5,6,7-tetrahydro-1-indenyl)ethane,1,3-propanedinyl-bis(4,5,6,7-tetrahydro)indene, propylene-bis(1-indene),isopropyl(1-indenyl) cyclopentadiene, diphenylmethylene(9-fluorenyl)cyclopentadiene and isopropylcyclopentadienyl-1-fluorene.

Another class of eligible compound (iii) according to the invention isrepresented by the formula

    (Cp).sub.r SiR.sup.3.sub.s X.sup.3.sub.4-r-s

wherein Cp is a cyclopentadienyl group; R³ is a hydrocarbon group of1-24, preferably 1-12, carbon atoms including an alkyl group such asmethyl, ethyl, propyl, butyl, pentyl, hexyl and octyl, an alkenyl groupsuch as vinyl and allyl, an aryl group such as phenyl, tolyl and xylyl,and an arallyl group such as benzyl, phenethyl, styryl and neophyl; X³is a halogen atom including fluorine, iodine, chlorine and bromine; andr and s are 0<r≦4 and 0≦s≦3, respectively, where r+s≦4.

Specific examples of the above compound (iii) includemonocyclopentadienyl silane, dicyclopentadienyl silane,tricyclopentadienyl silane, tetracyclopentadienyl silane,monocyclopentadienylmonomethyl silane, monocyclopentadienylmonoethylsilane, monocyclopentadienyldimethy silane, monocyclopentadienyldiethylsilane, monocyclopentadienyltrimethyl silane,monocyclopentadienyltriethyl silane, monocyclopentadienylmonomethoxysilane, monocyclopentadienylmonoethoxy silane,monocyclopentadienylmonophenoxy silane,monocyclopentadienylmonomethylmonochloro silane,monocyclopentadienylmonoethylmonochloro silane,monocyclopentadienylmonomethyldichloro silane,monocyclopentadienylmonoethyldichloro silane,monocyclopentadienyltrichloro silane, dicyclopentadienyldimethyl silane,dicyclopentadienyldiethyl silane, dicyclopentadienylmethylethyl silane,dicyclopentadienyldipropyl silane, dicyclopentadienylethylpropyl silane,dicyclopentadienyldiphenyl silane, dicyclopentadienylmethylphenylsilane, dicyclopentadienylmethylchloro silane,dicyclopentadienylethylchloro silane, dicyclopentadienyldichloro silane,dicyclopentadienylmonomethoxy silane, dicyclopentadienylmonoethoxysilane, dicyclopentadienylmonomethoxymonochloro silane,dicyclopentadienylmonoethoxymonochloro silane,tricyclopentadienylmonomethyl silane, tricyclopentadienylmonoethylsilane, tricyclopentadienylmonomethoxy silane,tricyclopentadienylmonoethoxy silane and tricyclopentadienylmonochlorosilane.

A further eligible compound (iii) is represented by the formula

(Ind)_(t) SiR⁴ _(u) X⁴ _(4-t-u)

wherein Ind is an indenyl group; R⁴ is a hydrocarbon group of 1-24,preferably 1-12, carbon atoms including an alkyl group such as methyl,ethyl, propyl, butyl, pentyl, hexyl and octyl, an alkenyl group such asvinyl and allyl, an aryl group such as phenyl, tolyl and xylyl, and anaralkyl group such as benzyl, phenethyl, styryl and neophyl; X⁴ is ahalogen atom including fluorine, iodine, chlorine and bromine; and t andu are 0≦t≦4 and 0≦u≦3, respectively, where t+u≦4.

Specific examples of the above compound (iii) include monoindenylsilane, diindenyl silane, triindenyl silane, tetraindenyl silane,monoindenylmonomethyl silane, monoindenylmonoethyl silane,monoindenyldimethyl silane, monoindenyldiethyl silane,monoindenyltrimethyl silane, monoindenyltriethyl silane,monoindenylmonomethoxy silane, monoindenylmonoethoxy silane,monoindenylmonophenoxy silane, monoindenylmonomethylmonochloro silane,monoindenylmonoethylmonochloro silane, monoindenylmonomethyldichlorosilane, monoindenylmonoethyldichloro silane, monoindenyltrichlorosilane, bisindenyldimethyl silane, bisindenyldiethyl silane,bisindenylmethylethyl silane, bisindenyldipropyl silane,bisindenyldiphenyl silane, bisindenylmethylphenyl silane,bisindenylmethylchloro silane, bisindenylethylchloro silane,bisindenyldichloro silane, bisindenylmonomethoxy silane,bisindenylmonoethoxy silane, bisindenylmonomethoxymonochloro silane,bisindenylmonoethoxymonochloro silane, triindenylmonoethyl silane,triindenylmonoethyl silane, triindenylmonomethoxy silane,triindenylmonoethoxy silane and triindenylmonochloro silane.

An inorganic carrier and/or particulate polymer carrier is used ascomponent (iv) of the catalyst composition. The inorganic carrier may beintrinsically in the form of particles, granules, flakes, foil orfibers, but, whatever the shape may be, should be 5-200 μm, preferably10-100 μm in maximum length. The inorganic carrier is preferably porous,having a surface area of 50-1,000 m² /g and a pore volume of 0.05-3 cm³.It may be chosen from the group of a carbonaceous material, a metal, ametal oxide, a metal chloride and a metal carbonate, or a mixturethereof, which is calcined usually at 200°-900° C. in the air, nitrogen,argon or other inert gas. Suitable metals for the inorganic carrier(iii) are aluminum and nickel. Eligible metal oxides are Group I-VIIImetal oxides of the Periodic Table including SiO₂, Al₂ O₃, MgO, CaO, B₂O₃, TiO₂, ZrO₂, Fe₂ O₃, SiO₂.Al₂ O₃, Al₂ O₃.MgO, Al₂ O₃.CaO, Al₂O₃.MgO.CaO, Al₂ O₃.MgO.SiO₂, Al₂ O₃.CuO, Al₂ O₃.Fe₂ O₃, Al₂ O₃.NiO andSiO₂.MgO. The double oxides are not particularly restricted in terms ofstructure and component ratio when used in the invention. The metaloxides may have adsorbed thereto small quantities of moisture and mayfurther contain a small amount of impurities.

The metal chloride used in the invention is a chloride of an alkalinemetal or alkaline earth metal, preferably MgCl₂ and CaCl₂. Examples ofthe metal carbonate are magnesium carbonate, calcium carbonate andbarium carbonate, while those of the carbonaceous material referred toherein are carbon black and activated carbon. The above metal oxides aremost preferred amongst the other inorganic carrier materials.

The term particulate polymer as used herein as a catalyst support orcarrier (iv) designates a solid particulate form of either thermoplasticor thermosetting resin having an average particle size 5-2,000 μm,preferably 10-100 μm, practically ranging from low molecular weight toultra high molecular weight polymers as long as these polymers remainsolid during the stages of catalyst preparation and polymerizationreaction. Specific examples of the particulate polymer include ethylenepolymers, ethylene alpha-olefin copolymers, propylene polymers orcopolymers, poly-1-butene and like polyolefins preferably of 2-12 carbonatoms, polyester, polyamide, polyvinylchloride, polymethylacrylate,polymethylmethacrylate, polystyrene, polynorbornen and naturallyoccurring polymers as well as mixtures thereof. The foregoing inorganicand particulate polymer carriers may be used per se as component (iv)according to the invention. Alternatively, they may be pretreated withan organoaluminum compound such as trimethylaluminum, triethylaluminum,triisobutylaluminum, tri-n-hexylaluminum, dimethylaluminum chloride,diethylaluminum chloride and diethylmonoethoxyaluminum, a modifiedorganoaluminum compound having Al--O--A bonds, or a silane compound.

The inorganic carrier may be used after treatment with an activehydrogen-containing compound such as alcohol and aldehydes, anelectron-donative compound such as ester and ether, or analkoxide-containing compound such as tetraalkoxysilicate,tetraalkoxyaluminum and transition-metal tetraalkoxide.

The carriers may be contacted with various pretreating compounds in anatmosphere of an inert gas such as nitrogen or argon in the presence ofan inert liquid hydrocarbon such as an aromatic hydrocarbon (6-12 carbonatoms) including benzene, toluene, xylene and ethylbenzene or analiphatic or alicyclic hydrocarbon (5-12 carbon atoms) includingheptane, hexane, decane, dodecane and cyclohexane, with or withoutstirring at -100° to 200° C., preferably -50° to 100° C. for 30 minutesto 50 hours, preferably 1-24 hours. This pretreatement reaction iscarried out preferably in the presence of a solvent of an aromatichydrocarbon such as benzene, toluene, xylene and ethylbenzene in whichthe pretreating compounds are rendered soluble. The resulting carriermay be readily put to use for the preparation of catalyst componentswithout having to remove the solvent. If the pretreating compound, forexample a modified organoaluminum compound, is insoluble or hardlysoluble, there may be added pentene, hexane, decane, dodecane orcyclohexane to allow the reaction product to precipitate and thereafterdry. Alternatively, part or all of the aromatic hydrocabon solvent maybe removed as by means of drying.

There is no particular restriction imposed upon the ratio ofcarrier/pretreating compound, the latter being usually 1-10,000millimoles, preferably 5-1,500 millimoles per 100 grams carrier.

The various components (i)-(iv) used in the invention may be contactedin the following older:

(1) Components (i) through (iv) are all simultaneously contactedtogether.

(2) Components (i), (ii) and (iii) are contacted together and thereafterwith component (iv).

(3) Components (ii), (iii) and (iv) are contacted together andthereafter with component (i).

(4) Components (i), (iii) and (iv) are contacted together and thereafterwith component (ii).

(5) Components (i), (ii) and (iv) are contacted together and thereafterwith component (iii).

(6) Components (i) and (ii) are contacted together, then with component(iii) and thereafter with component (iv).

(7) Components (i) and (ii) are contacted together, then with component(iv) and thereafter with component (iii).

(8) Components (i) and (iii) are contacted together, then with component(ii) and thereafter with component (iv).

(9) Components (i) and (iii) are contacted together, then with component(iv) and thereafter with component (ii).

(10) Components (i) and (iv) are contacted together, then with component(ii) and thereafter with component (iii).

(11) Components (i) and (iv) are contacted together, then with component(iii) and thereafter with component (ii).

(12) Components (ii) and (iii) are contacted together, then withcomponent (i) and thereafter with component (iv).

(13) Components (ii) and (iii) are contacted together, then withcomponent (iv) and thereafter with component (i).

(14) Components (ii) and (iv) are contacted together, then withcomponent (i) and thereafter with component (iii).

(15) Components (ii) and (iv) are contacted together, then withcomponent (iii) and thereafter with component (i).

(16) Components (iii) and (iv) are contacted together, then withcomponent (i) and thereafter with component (ii).

(17) Components (iii) and (iv) are contacted together, then withcomponent (ii) and thereafter with component (i).

(18) Components (i) and (iv) are contacted together, then with component(ii) and thereafter with component (iii).

(19) Components (i) and (iv) are contacted together, then with component(iii) and thereafter with component (ii).

It has now been found that the sequences (1), (2), (5), (7) and (8)above are most effective.

These four components (i) through (iv) may be, not restrictively,contacted in an atmosphere of an inert gas such as nitrogen or argon inthe presence of ah inert liquid hydrocarbon such as an aromatichydrocarbon (6-12 carbon atoms) including benzene, toluene, xylene andethylbenzene, or an aliphatic or alicyclic hydrocarbon (5-12 carbonatoms) including heptane, hexane, decane, dodecane and cyclohexane, withor without stirring at -100° to 200° C., preferably -50° to 100° C. for30 minutes to 50 hours, preferably 1-24 hours. It is to be noted howeverthat the reaction is conducted under conditions to retain the polymercarrier material substantially in a solid state.

Amongst the listed solvents are used most advantageously the aromatichydrocarbons because the components (i), (ii) and (iii) are all solubletherein. Reference is made to the earlier mentioned procedures ofpretreating the carrier materials for the utilization or disposal of theinert hydrocarbon solvents commonly used.

Component (ii) is used in an amount of 0.01-1,000 moles, preferably0.1-100 moles, more preferably 1-10 moles per mole of component (i).Component (iii) is used in an amount of 0.01-100 moles, preferably0.1-10 moles, more preferably 1-5 moles per mole of component (i).Component (i) is used in an amount by transition-metal concentration(Me¹)of 0.01-500 millimoles, preferably 0.05-200 millimoles, morepreferably 0.1-20 millimoles per 100 g of carrier (iv). The catalystcomponents used in the invention should have an atomic ratio of Al/Me¹in the range of 0.1-2,000, preferably 15-1,000.

The term modified organoaluminum compound (II) is used herein todesignate a reaction product of an organoaluminum compound and waterwhich has 1-100, preferably 1-50 Al--O--Al bonds in the molecule. Thisreaction is usually conducted in the presence of an inert hydrocarbonsuch as pentane, hexane, keptane, cyclohexane, methylcyclohexane,benzene, toluene and xylene, of which aliphatic and aromatichydrocarbons are preferred. The starting organoaluminum compound may berepresented by the formula

    R.sup.5.sub.v AlX.sup.5.sub.3-v

where R⁵ is an alkyl, alkenyl, aryl or aralkyl group having a carbonnumber of 1-18, preferably 1-12; X⁵ is a hydrogen or halogen atom; and vis an integer of 1≦v≦3.

The above compound is typically exemplified by trialkylaluminum havingan alkyl group optionally such as methyl, ethyl, propyl, isopropyl,butyl, isobutyl, pentyl, hexyl, octyl, decyl and dodecyl groups, ofwhich methyl group is particularly preferred.

The water/organoaluminum reaction takes place in a molar ratio ofwater:Al in the range of 0.25:1-1.2:1, preferably 0.5:1-1:1 at atemperature of usually -70° to 100° C., preferably -20° to 20° C., for aperiod of 5-24 hours, preferably 5-10 hours. As water for reaction withthe organoaluminum compound, there may be used crystal water containedin hydrates of copper sulfate or aluminum sulfate.

The catalyst component (I) and the modified organoaluminum compound (II)may be supplied separately or as an admixture to the polymerizationreaction system. In either case, they are used in a ratio such that theatomic ratio of aluminum in the organoaluminum compound (II) totransition metal in the catalyst component (I) remain in the range of1-100,000, preferably 5-1,000.

The term olefins as used herein designates alpha-olefins, cyclicolefins, dienes, trienes and styrene analogs. Alpha-opefins have acarbon number of 2-12, preferably 2-8 and typically include ethylene,propylene, butene-1, hexane-1 and 4-methylpentene-1. These olefins maybe homopolymerized or copolymerized such as by alternating, random orblock copolymerization process.

The inventive process may be effectively applied where a diene compoundsuch as butadiene, 1,4-hexadiene, ethylidene norbornene anddicyclopentadiene is used to reform the polymer product. In such acopolymerization reaction for example of ethylene and an alpha-olefin of3-12 carbon atoms, it is desirable to hold an alpha-olefin content inthe ethylene/alpha-olefin copolymer to 40 mole % or less, preferably 30mole % or less, more preferably 20 mole % or less.

The polymerization reaction according to the invention is conducted in aslurry, solution or gase phase in the presence or absence of an inerthydrocarbon solvent such as an aliphatic hydrocarbon including hexaneand heptane, an aromatic hydrocarbon including benzene, toluene andxylene, and an alicyclic hydrocarbon including cyclohexane, andmethylcyclohexane, substantially without the presence of oxygen andwater, at a temperature of 20°-200° C., preferably 50°-100° C. under apressure of atmospheric -70 kg/cm² G, preferably atmospheric -20 kg/cm²G, for a time length of 5 minutes to 10 hours, preferably 5 minutes to 5hours.

Whilst the molecular weight of the polymer product obtained may beadjusted to some extent by varying the polymerization temperature, themolar ratio of the catalyst and other polymerization parameters, it canbe more effectively adjusted by introducing hydrogen into the reactionsystem.

The inventive process can be advantageously used also in multi-stagepolymerizations where hydrogen concentration and reaction temperaturevary.

The invention will be further described by way of the followingexamples.

Preparation of Modified Organoaluminum Compound (Methylalmoxane)

A 300-ml three-necked flask equipped with an electromagnetic stirrer wascharged with 13 grams of copper sulfate heptahydrate and 50 ml oftoluene. The admixture after being suspended was added at 0° C. and over2 hours with droplets of 150 ml of a 1 mmol/ml triethylaluminumsolution. The reaction was effected at 25° C. for 24 hours. Filtrationof the reaction mixture and subsequent evaporation of excess toluenegave 4 grams of methylalmoxane (MAO) in the form of a white crystal.

Preparation of Catalyst Component A

(1) Pretreatment of Carrier (iv)

A 300 cc three-necked flask was charged with 100 ml refined toluene and10 g SiO₂ (surface area 300 m² /g, Grade No. 952 of Fuji Davison) whichhad been calcined at 460° C. for 5 hours in nitrogen atmosphere,followed by addition of 6 ml toluene solution of methylalmoxane(concentration 2.5 mmol/ml). The admixture was stirred at roomtemperature for 2 hours and thereafter dried by nitrogen blow to yield afluid particulate product.

(2) Preparation of Transition Metal Catalyst

    Component  Components (i)+(ii)+(iii)!

A 300 cc three-necked flask was charged with 100 ml refined toluene, 50ml tetrahydrofuran (THF) solution of ethylmagnesium chloride (EtMgCl)(concentration 2 mols/l) and 2.2 g indene and cooled at -60° C. Aseparate flask was charged with 50 ml toluene, 4.2 gtetrapropoxyzirconium (Zr(OPr)₄) and 0.8 g indene. This solution was fedinto the first flask, and the whole mixture therein was stirred at -60°C. for 1 hour, followed by heating with continued stirring up to 20° C.slowly over 2 hours. The reaction was continued at 45° C. for 3 hours.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

A 300 cc three-necked flask was charged with 10 g carrier prepared asabove in nitrogen atmosphere and 30 ml toluene solution of transitionmetal catalyst component prepared as above, followed by 15 ml refinedtoluene. The admixture was stirred at room temperature for 2 hours,followed by removal of the solvent by nitrogen blow in vacuum therebyobtaining 11 g solid catalyst component A.

Preparation of Catalyst Component B

(1) Pretreatment of Carrier (iv)

The same as for catalyst component A.

(2) Preparation of Transition Metal Catalyst

    Component  Components (i)+(ii)+(iii)!

A 300 cc three-necked flask was charged with 100 ml refined toluene, 9.8g triethylboron (ET₃ B) and 2.5 g cyclopentadiene and cooled at -60° C.A separate flask was charged with 4.2 g tetrapropoxyzirconium and 0.84cyclopentadiene. The rest of the procedure was the same as in thepreparation of Component A.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

A 300 cc three-necked flask was charged with 10 g carrier prepared asabove in nitrogen atmosphere and 35 ml toluene solution of transitionmetal catalyst component prepared as above, followed by addition of 15ml refined toluene. The admixture was stirred at room temperature for 2hours, followed by removal of the solvent by nitrogen blow in vacuumthereby obtaining solid catalyst component B.

Preparation of Catalyst Component C

(1) Carrier (iv)

10 g SiO₂ (surface area 300 m² /g, Grade No. 952 of Fuji Davison) wasused, which had been calcined at 600° C. for 5 hours. This carrier wasnot pretreated.

(2) Preparation of Transition Metal Catalyst

    Component  Components (i)+(ii)+(iii)!

A 300 cc three-necked flask was charged with 100 ml refined toluene, 25ml tetrahydrofuran solution of n-butylmagnesium chloride (concentration2 mols/l) and 1.7 g cyclopentadiene and stirred at room temperature for30 minutes, followed by addition over 20 minutes of 4.2 gtetrapropoxyzirconium dissolved in 50 ml toluene. The reaction wascontinued at 45° C. for 3 hours.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

A 300 cc three-necked flask was charged with 10 g carrier prepared asabove in nitrogen atmosphere and 29 ml toluene solution of transitionmetal catalyst component prepared as above, followed by addition of 15ml refined toluene. The admixture was stirred at room temperature for 2hours, followed by removal of the solvent by nitrogen blow in vacuumthereby obtaining solid catalyst component C.

Preparation of Catalyst Component D

(1) Pretreatment of Carrier (iv)

A 400 ml stainless steel pot containing 25 pieces of half inch stainlesssteel balls was charged with 10 g magnesium anhydrous chloride and 3.8 gtriethoxyaluminum. The admixture was subjected to ball-milling innitrogen atmosphere at room temperature.

(2) Preparation of Transition Metal Catalyst

    Component  Components (i)+(ii)+(iii)!

A 300 cc three-necked flask was charged with 100 ml refined toluene,15.7 g of diethylzinc (Et₂ Zn) and 5.9 g indene and stirred at roomtemperature for 30 minutes. 4.2 g tetrapropoxyzirconium dissolved in 50ml toluene was added over 20 minutes. The reaction was continued at 45°C. for 3 hours.

(3) Preparation of Solid Catalyst Component

Components (i)+(ii)+(iii)+(iv)!

A 300 cc three-necked flask was charged with 10 g carrier prepared asabove in nitrogen atmosphere and 27 ml toluene solution of transitionmetal catalyst component prepared as above, followed by addition of 15ml refined toluene. The admixture was stirred at room temperature for 2hours, followed by removal of the solvent by nitrogen blow in vacuumthereby obtaining solid catalyst component D.

Preparation of Catalyst Component E

(1) Pretreatment of Carrier (iv)

10 g polyethylene powder dried at 60° C. for 3 hours (MFR 1.0 g/10 min,bulk density 0.41 g/cc, particle size 500 μm, melting point 121° C.) wasadded dispersively with 6 ml toluene solution of methylalmoxane(concentration 2.5 mmol/ml). The admixture was stirred at roomtemperature for 1 hour, followed by drying with nitrogen blow therebyobtaining a fluid particulate product.

(2) Preparation of Transition Metal Catalyst

    Component  Components (i)+(ii)+(iii)!

The procedure for the preparation of Catalyst Component A was followedexcept that 64 ml tetrahydrofuran solution of ethylmagnesium bromide(EtMgBr) (concentration 2 mols/l).

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

A 300 cc three-necked flask was charged with 10 g carrier prepared asabove in nitrogen atmosphere and 38 ml toluene solution of transitionmetal catalyst component prepared as above, followed by addition of 15ml refined toluene. The admixture was stirred at room temperature for 2hours, followed by removal of the solvent by nitrogen blow in vacuumthereby obtaining solid catalyst component E.

Preparation of Catalyst Component F

(1) Pretreatment of Carrier (iv)

The procedure for the preparation of Catalyst Component A was followedexcept that 10 g Al₂ O₃ (surface area 300 m² /g and average particlesize 60 μm) was used, which had been calcined at 400° C. for 5 hours.

(2) Preparation of Transition Metal Catalyst

    Component  Components (i)+(ii)+(iii)!

A 300 cc three-necked flask was charged with 100 ml refined toluene, 64ml THF solution of ethylmagnesium chloride (concentration 2 mols/l) and4.0 g methylcyclopentadiene. The admixture was stirred at roomtemperature for 30 minutes, followed by addition over 20 minutes of 4.9g tetrabutoxyzirconium (Zr(OBu)₄) dissolved in 50 ml toluene. Thereaction was continued with stirring at 45° C. for 3 hours.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

The procedure for Catalyst Component A was followed except that theabove solution of transition metal component was mixed with the carrier(iv) such that Zr deposits were 2.1 wt %.

Preparation of Catalyst Component G

(1) Pretreatment of Carrier (iv)

The procedure for the preparation of Catalyst Component A was followedexcept that 15 ml n-hexane solution of trimethylaluminum (AlMe₃)(concentration 1 mmol/ml) was used.

(2) Preparation of Transition Metal Catalyst

    Component  Components (i)+(ii)+(iii)!

A 300 cc three-necked flask was charged with 100 ml refined toluene, 64ml THF solution of ethylmagnesium chloride (2 mols/l) and 3.4cyclopentadiene. The admixture was stirred at room temperature for 30minutes, followed by addition over 20 minutes of 3.9 gtripropoxychlorozirconium (Zr(OPr)₃ Cl) dissolved in 50 ml toluene. Thereaction was continued with stirring at 45° C. for 3 hours.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

The procedure for Catalyst Component A was followed except that theabove solution of transition metal component was mixed with the carrier(iv) such that the amount of Zr deposits was 2 wt %.

Preparation of Catalyst Component H

(1) Pretreatment of Carrier (iv)

The same as for Catalyst Component A.

(2) Preparation of Transition Metal Catalyst

    Component  Components (i)+(ii)+(iii)!

A 300 cc three-necked flask was charged with 100 ml refined toluene, 26ml THF solution of ethylmagnesium chloride (concentration 2 mol/l) and6.6 g bisindenylethane. The admixture was stirred at room temperaturefor 30 minutes, followed by addition over 20 minutes of 3.5 gtetraethoxyzirconium (Zr(OEt)₄) dissolved in 50 ml toluene. The reactionwas continued with stirring at 45° C. for 3 hours.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

The procedure for Catalyst Component A was followed except that theabove solution of transition metal component was mixed with the abovecarrier (iv) such that Zr deposits were 1.9 wt %.

Preparation of Catalyst Component I

(1) Pretreatment of Carrier (iv)

The same as for Catalyst Component A.

(2) Preparation of Transition Metal Catalyst

    Component  Components (i)+(ii)+(iii)!

The procedure for Catalyst Component H was followed except that 4.8 gbiscyclopentadienyldimethyl silane was used.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

The procedure for Catalyst Component A was followed except that theabove solution of transition metal component was mixed with the abovecarrier (iv) such that Zr deposits were 1.9 wt %.

Preparation of Catalyst Component J-P

(1) Pretreatment of Carrier (iv)

The same as for Catalyst Component A.

(2) Preparation of Transition Metal Catalyst

    Component  Component (i)+(ii)+(iii)!

The transition metal catalyst components prepared are shown andidentified in Table 1.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

The procedure for Catalyst Component A was followed to obtain CatalystComponents J-P having respective metal deposits as shown in Table 1.

Preparation of Catalyst Component A'

(1) Pretreatment of Carrier (iv)

A 300 cc three-necked flask was charged with 100 ml refined toluene and10 g SiO₂ (surface area 300 m² /g, Grade No. 952 of Fuji Davison) whichhad been calcined at 460° C. for 5 hours in nitrogen atmosphere,followed by addition of 6 ml toluene solution of methylalmoxane(concentration 2.5 mmol/ml). The admixture was stirred at roomtemperature for 2 hours and thereafter dried by nitrogen blow to yield afluid particulate product.

(2) Preparation of Transition Metal Catalyst

    Component  Components (i)+(ii)+(iii)!

A 300 cc three-necked flask was charged with 100 ml refined toluene,5.84 g triethylaluminum (AlEt₃) and 2.2 g indene and cooled at -60° C. Aseparate flask was charged with 50 ml toluene, 4.2 gtetrapropoxyzirconium (Zr(OPr)₄) and 0.8 g indene. This solution was fedinto the first flask, and the whole mixture therein was stirred at -60°C. for 1 hour, followed by heating with continued stirring up to 20° C.slowly over 2 hours. The reaction was continued at 45° C. for 3 hoursuntil there was obtained a black solution containing 0.075 mmol/ml Zr.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

A 300 cc three-necked flask was charged with 10 g carrier prepared asabove in nitrogen atmosphere and 30 ml toluene solution of transitionmetal catalyst component prepared as above, followed by addition of 15ml refined toluene. The admixture was stirred at room temperature for 2hours, followed by removal of the solvent by nitrogen blow in vacuumthereby obtaining 11 g solid catalyst component A'.

Preparation of Catalyst Component B'

(1) Pretreatment of Carrier (iv)

The same as for catalyst component A'.

(2) Preparation of Transition Metal Catalyst

    Component  Components (i)+(ii)+(iii)!

A 300 cc three-necked flask was charged with 100 ml refined toluene,5.84 g triethylaluminum (AlEt₃) and 0.60 g cyclopentadiene and cooled at-60° C. A separate flask was charged with 50 ml toluene, 4.2 gtetrapropoxyzirconium and 0.24 g cyclopentadiene. The rest of theprocedure was the same as in the preparation of Component A'.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

The same as for Catalyst Component A'.

Preparation of Catalyst Component C'

(1) Carrier (iv)

The same SiO₂ as in Catalyst Component A' was used. This carrier was notpretreated.

(2) Preparation of Transition Metal Catalyst

    Component  Components (i)+(ii)+(iii)!

A 300 cc three-necked flask was charged with 100 ml refined toluene,13.3 g diethylaluminum ethoxide AlEt₂ (OEt)! and 2.4 g cyclopentadieneand cooled at -60° C. A separate flask was charged with 50 ml toluene,4.2 g Zr(OPr)₄ and 1.0 g cyclopendadiene. The rest of the procedure wasthe same as in the preparation of Component A'.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

The same as for Catalyst Component A'.

Preparation of Catalyst Component D'

(1) Pretreatment of Carrier (iv)

In place of silica, there was used alumina Al₂ O₃ (surface area 300 m²/g and average particle size 60 μm) which was pretreated as per CatalystComponent A'.

(2) Preparation of Transition Metal Catalyst

    Component  Components (i)+(ii)+(iii)!

A 300 cc three-necked flask was charged with 100 ml refined toluene,5.84 g triethylaluminum and 2.53 g methylcyclopentadiene and cooled at-60° C. A separate flask was charged with 50 ml toluene, 4.93 g Zr(OBu)₄and 1 g methylcyclopentadiene. The rest of the procedure was the same asin the preparation of Component A'.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

The same as for Catalyst Component A'.

Preparation of Catalyst Component E'

(1) Pretreatment of Carrier (iv)

A 400 ml stainless steel pot containing 25 pieces of half inch stainlesssteel balls was charge with 10 g magnesium anhydrous chloride and 3.8 gtriethoxyaluminum. The admixture was subjected to ball-milling innitrogen atmosphere at room temperature. 10 g milled product was used asthe carrier.

(2) Preparation of Transition Metal Catalyst

    Component  Components (i)+(ii)+(iii)!

The same as for Catalyst Component A'.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

The same as for Catalyst Component A'.

Preparation of Catalyst Component F'

(1) Pretreatment of Carrier (iv)

A 300 ml three-necked flask was charged with 100 ml refined toluene, 10g polyethylene powder (MFR 1.0/10 min, density 0.9210 g/cm³, bulkdensity 0.41 g/cc, particle size 500 μm and melting point 121° C.) and 6ml toluene solution of methylalmoxane which was uniformly dispersed overthe polyethylene powder in nitrogen atmosphere.

(2) Preparation of Transition Metal Catalyst

    Component  Components (i)+(ii)+(iii)!

A 300 cc three-necked flask was charged with 100 ml refined toluene, 5.8g triethylaluminum, 3 g indene and 4.2 g Zr(OPr)₄ in nitrogen atmosphereat room temperature. The admixture was stirred at 45° C. for 2 hours.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

The same as for Catalyst Component A'.

Preparation of Catalyst Component G'

(1) Pretreatment of Carrier (iv)

The procedure for the preparation of Catalyst Component A' was followedexcept that silica.alumina (surface area 300 m² /g, pore volume 0.7 cc/gand average particle size 50 μm) was used in place of silica.

(2) Preparation of Transition Metal Catalyst

    Component  Components (i)+(ii)+(iii)!

A 300 cc three-necked flask was charged with 150 ml refined toluene,15.4 g Al Et₂ Cl, 4.2 g Zr(OPr)₄ and 3.4 g cyclopentadiene in nitrogenatmosphere at room temperature. The admixture was stirred at 45° C. for2 hours.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

The same as for Catalyst Component A'.

Preparation of Catalyst Component H'

(1) Pretreatment of Carrier (iv)

The same as for Catalyst Component A'.

(2) Preparation of Transition Metal Catalyst

    Component  Components (i)+(ii)+(iii)!

A 300 cc three-necked flask was charged with 50 ml refined toluene, 5.84g triethylaluminum, 4.85 g biscyolopentadienyldimethylsilane, and 3.5 gZr(OEt)₄ in nitrogen atmosphere at room temperature. The admixture wasstirred at 45° C. for 2 hours.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

The same as for Catalyst Component A'.

Preparation of Catalyst Component I'

(1) Pretreatment of Carrier (iv)

The same as for Catalyst Component A'.

(2) Preparation of Transition Metal Catalyst

    Component  Components (i)+(ii)+(iii)!

A 300 cc three-necked flask was charged with 150 ml refined toluene,5.84 g triethylaluminum, 3.7 g biscyclopentadienylmethane and 4.2 gZr(OPr)₄ in nitrogen atmosphere at room temperature. The admixture wasstirred at 45° C. for 2 hours.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

The same as for Catalyst Component A'.

Preparation of Catalyst Component J'

(1) Pretreatment of Carrier (iv)

The procedure for Catalyst Component A' was followed except that 15 mltoluene solution of trimethylaluminum (concentration 1 mmol/ml) was usedin place of methylalmoxane.

(2) Preparation of Transition Metal Catalyst

    Component  Component (i)+(ii)+(iii)!

A 300 cc three necked flask was charged with 150 ml refined toluene,11.7 g triethylaluminum, 13.4 g bisindenylethane and 3.9 g Zr(OPr)₄ Clin nitrogen atmosphere at room temperature. The admixture was stirred at45° C. for 2 hours.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

The procedure for Catalyst Component A' was followed.

Preparation of Catalyst Component K'

(1) Pretreatment of Carrier (iv)

The same as for catalyst component A'.

(2) Preparation of Transition Metal Catalyst

    Component  Components (i)+(ii)+(iii)!

3 g zirconium tetrachloride was admixed with an ether solution ofmagnesium benzylchloride and let alone at -20° C. for 2 hours, followedby stirring at room temperature for 2 hours. Byproduced MgCl₂ wasremoved, and the ether solution was concentrated and cooled to -20° C.until there was obtained a crystalline product (ZrBz₄) having a meltingpoint of 112.8° C.

A 300 cc three-necked flask was charged with 150 ml refined toluene,14.6 g triethylaluminum, 2.54 g cyclopentadiene and 5.8 g ZrBz₄. Theadmixture was stirred at 45° C. for 2 hours.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

The same as for Catalyst Component A'.

Preparation of Catalyst Component L'

(1) Pretreatment of Carrier (iv)

The same as for catalyst component A'.

(2) Preparation of Transition Metal Catalyst

    Component  Components (i)+(ii)+(iii)!

The procedure for Catalyst Component K' was followed except thattitanium tetrachloride was used in place of zirconium tetrachloride toproduce TiBz₄.

A 300 cc three-necked flask was charged with 150 ml refined toluene,14.6 g triethylaluminum, 5.2 g pentamethylcyclopentadiene and 5.3 gTiBz₄ in nitrogen atmosphere. The admixture was stirred at 45° C. for 2hours.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

The same as for Catalyst Component A'.

Preparation of Catalyst Component M'

(1) Pretreatment of Carrier (iv)

The same as for catalyst component A'.

(2) Preparation of Transition Metal Catalyst

    Component  Components (i)+(ii)+(iii)!

The procedure for Catalyst Component K' was followed except that hafniumtetrachloride was used in place of ZrBz₄ to produce HfBz₄.

A 300 cc three-necked flask was charged with 150 ml refined toluene,14.6 g triethylaluminum, 2.54 g cyclopentadiene and 5.8 g ZrBz₄. Theadmixture was stirred at 45° C. for 2 hours.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

The same as for Catalyst Component A'.

Preparation of Catalyst Component N'

(1) Pretreatment of Carrier (iv)

The procedure for Catalyst Component A' was followed except that 15 mlhexane solution of Zr(OPr)₄ (concentration 1 mmol/ml) was used in placeof methylalmoxane.

(2) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

A 300 cc three-necked flask was charged-with 10 g carrier prepared asabove, 100 ml refined n-hexane, 0.84 g triethylaluminum and 0.12 gcyclopentadiene. The admixture was stirred at room temperature for 2hours, followed by addition of 0.5 g Zr(OEt)₄, and thereafter stirred at45° C. for 2 hours in nitrogen atmosphere. The solvent was removed bynitrogen blow in vacuum.

Preparation of Catalyst Component O'

(1) Pretreatment of Carrier (iv)

The procedure for Catalyst Component A' was followed except that 10 gMg(CO₃)₂ powder dried at 150° C. for 2 hours was used in place ofsilica.

(2) Preparation of Transition Metal Catalyst

The same as for Catalyst Component A'.

(3) Preparation of Solid Catalyst Component

     Components (i)+(ii)+(iii)+(iv)!

The same as for Catalyst Component A'.

INVENTIVE EXAMPLE 1

A 3-liter stainless steel autoclave equipped with stirrer was purgedwith nitrogen and thereafter supplied with 200 g of dry salt, 22 ml of 1mmol/ml methylalmoxane solution and 100 mg of Catalyst Component A. Theadmixture was heated at 60° C. with stirring. A mix of ethylene andbutene-1 gases (butene-1/ethylene molar ratio 0.25) was charged to bringthe reactor pressure up to 9 kgf/cm² G, whereupon polymerizationreaction was initiated and continued for 1 hour with continued charge ofa mixed gas of ethylene and butene-1 (butene-1/ethylene molar ratio0.05) to maintain the reaction system at 9 kgfr/cm² G.

Upon completion of the reaction, excess gas was removed from the reactorwhich was then cooled to yield 66 grams of a white polymer.

INVENTIVE EXAMPLES 2-16

The procedure of Inventive Example 1 was followed for the polymerizationunder the conditions shown in Table 1 and with the results shown inTable 2.

INVENTIVE EXAMPLE 17

The procedure of Inventive Example 1 was followed for homopolymerizationof ethylene under the conditions indicated in Table 1 and with theresults shown in Table 2, except that an ethylene gas was used forpressure control in place of a mixed gas of ethylene and butene-1.

INVENTIVE EXAMPLE 18

The procedure of Inventive Example 1 was followed except that propylenegas was used in the homopolymerization of propylene and that thereaction temperature and pressure were 50° C. and 7 kgf/cm² G,respectively.

Comparative Example 1-3

The procedure of Inventive Example 1 was followed under the conditionsshown in Table 1 and with the results in Table 2.

INVENTIVE EXAMPLE 19

A 3-liter stainless steel autoclave equipped with stirrer was purgedwith nitrogen and thereafter supplied with 200 g of dry salt, 22 ml of 1mmol/ml methylalmoxane solution and 100 mg of Catalyst Component A'. Theadmixture was heated at 60° C. with stirring. A mix of ethylene andbutene-1 gases (butene-1/ethylene molar ratio 0.25) was charged to bringthe reactor pressure up to 9 kgf/cm² G, whereupon polymerizationreaction was initiated and continued for 1 hour with continued charge ofa mixed gas of ethylene and butene-1 (butene-1/ethylene molar ratio0.05) to maintain the reaction system at 9 kgfr/cm² G.

Upon completion of the reaction, excess gas was removed from the reactorwhich was then cooled to yield 76 grams of a white polymer.

Table 2 shows the polymerization results and the properties of resultantpolymers (Inventive Examples 1-18 and Comparative Examples 1-3).

INVENTIVE EXAMPLES 20-35

The procedure of Inventive Example 19 was followed that CatalystComponents B'-O' were used in place of Catalyst Component A' asindicated in Table 3.

Comparative Examples 4-6

The procedure of Inventive Example 19 was followed except that CatalystComponents T, U and V were used in place of Catalyst Component A'.

Table 4 shows the polymerization results and the properties of resultantpolymers (Inventive Examples 19-35 and Comparative Examples 4-6).

Each of the polymers obtained in the respective Inventive andComparative Examples was subjected to the following tests.

Melt Index (MI)

The procedure of ASTM D1238-57T was followed.

Density (D)

The procedure of ASTM D1505-68 was followed.

Melting Point by Calorimetry (DSC)

5 mg of the polymer sample was disposed at 180° C. for 3 minutes, cooledto 0° C. over 10° C./min and allowed to stand at 0° C. for 10 minutes,followed by heating with a temperature rise of 10° C./min with use of amelting point tester (Seiko Electronics DSC-20).

                                      TABLE 1                                     __________________________________________________________________________                                                     amount of                                                                     addition during                                                    composition                                                                         transition                                                                         polymerization                       solid catalyst component      ratio metal                                                                              transition                   Catalyst                                                                              carrier  component                                                                            component                                                                             component                                                                           (i):(iii):(ii)                                                                      deposits                                                                           metal                                                                              modified                                                                           Al/Me              lot     (iv)     (i)    (iii)   (ii)  mol ratio                                                                           wt % mg   Al   ratio              __________________________________________________________________________    IE 1                                                                              A   SiO.sub.2 -MAO                                                                         Zr(OPr).sub.4                                                                        indene  EtMgCl                                                                              1:4:8 2    1.9  MAO  1000               2   B    "       "      cyclopentadiene                                                                       Et.sub.3 B                                                                           "    "    2.0  "    "                  3   C   SiO.sub.2                                                                              "       "      nBuMgCl                                                                             1:2:4 1.9  1.8  "    "                  4   D   MCl.sub.2 -Al(OEt).sub.3                                                               "      indene  Et.sub.2 Zn                                                                         1:4:10                                                                              1.8  1.7  "    "                  5   E   PE polymer-MAO                                                                         "       "      EtMgBr                                                                               "    2.0  1.9  "    "                  6   F   Al.sub.2 O.sub.3                                                                       Zr(OBu).sub.4                                                                        methylcyclo-                                                                           "     "    "    2.1  "    "                                          pendadiene                                            7   G   SiO.sub.2 -AlMe.sub.3                                                                  Zr(OPr).sub.3 Cl                                                                     cyclopentadiene                                                                       EtMgCl                                                                               "    "    1.7  "    "                  8   H   SiO.sub.2 -MAO                                                                         Zr(OEt).sub.4                                                                        bis-indenyl-                                                                           "    1:2:4 1.9  1.8  "    "                                          ethane                                                9   I    "       "      bis-cyclo-                                                                             "     "    "    1.9  "    "                                          pendadienyl-                                                                  dimethyl silane                                       10  J    "       "      bis-cyclopenta-                                                                        "     "    "    1.8  "    "                                          dienyl metane                                         11  K   SiO.sub.2 -MAO                                                                         (1)Ti(OBu).sub.3 Cl                                                                  cyclopendadiene                                                                       EtMgCl                                                                              1:3:10                                                                              2.0  2.3  MAO  1000               12  L    "       ZrBz.sub.4                                                                            "       "    1:4:8 "    1.9  "    "                  13  M    "       (2)Zr(neophil).sub.4                                                                 pentamethyl-                                                                           "     "    "    1.7  "    "                                          cyclopendadiene                                       14  N    "       ZrCl.sub.4                                                                           cyclopendadiene                                                                       EtLi  1:2:6 "    2.1  "    "                  15  O    "       TiCl.sub.4                                                                            "      EtMgCl                                                                              1:2:4 "    2.0  "    "                  16  P    "       Hf(OPr).sub.4                                                                         "       "    1:4:8 "    2.4  "    "                  17  H    "       Zr(OEt).sub.4                                                                        bis-indenyl-                                                                           "    1:2:4 1.9  1.8  "    "                                          ethane                                                18  H    "        "     bis-indenyl-                                                                           "     "    "    "    "    "                                          ethane                                                CE 1                                                                              Q    --      Zr(OPr).sub.4                                                                        indene  EtMgCl                                                                              1:4:8 --   1.7  "    "                  2   R   SiO.sub.2 -MAO                                                                          "      --      "    1:0:7 2    1.6  "    "                  3   S    "        "     indene   --   1:4:0 "    1.5  "    "                  __________________________________________________________________________     IE: Inventive Example                                                         CE: Comparative Example                                                       (1) trin-butoxymonochlorotitanium                                             (2) tetraneophyl zirconium                                               

                  TABLE 2                                                         ______________________________________                                                 catalytic         bulk   polymer                                                                             melting                               yield    activity MFR      density                                                                              density                                                                             point                                 g        g/g Me   g/10 min g/cc   g/cm.sup.3                                                                          °C.                            ______________________________________                                        IE 1  66     35,000   0.8    0.39   0.9210                                                                              114.0                               2     102    51,000   4.8    0.40   0.9215                                                                              104.7                               3     82     46,000   5.1    0.38   0.9220                                                                              106.8                               4     62     37,000   0.6    0.35   0.9119                                                                              113.0                               5     74     39,000   0.4    0.33   0.9117                                                                              112.8                               6     90     43,000   2.1    0.41   0.9213                                                                              104.1                               7     97     57,000   3.8    0.37   0.9225                                                                              106.3                               8     90     50,000   1.1    0.42   0.9218                                                                              108.7                               9     74     39,000   3.9    0.38   0.9119                                                                              103.8                               10    52     29,000   2.5    0.39   0.9220                                                                              103.1                               11    53     23,000   3.7    0.36   0.9208                                                                              104.1                               12    59     31,000   8.4    0.35   0.9116                                                                              101.1                               13    70     41,000   7.9    0.38   0.9218                                                                              107.3                               14    69     33,000   12.2   0.39   0.9231                                                                              108.0                               15    56     28,000   4.7    0.39   0.9222                                                                              106.9                               16    50     21,000   3.2    0.34   0.9210                                                                              103.9                               17    106    59,000   2.8    0.41   0.9508                                                                              135.1                               18    56     31,000   2.0    0.37   0.9021                                                                              138.9                               CE 1  114    67,000   0.8    0.24   0.9196                                                                              113.0                               2      0        0     --     --     --    --                                  3     17     11,000   1.3    0.40   0.9280                                                                              115.8                               ______________________________________                                    

                                      TABLE 3                                     __________________________________________________________________________                                                     amount of                                                                     addition during                                                    composition                                                                         transition                                                                         polymerization                       solid catalyst component      ratio metal                                                                              transition                   Catalyst                                                                              carrier  component                                                                            component                                                                             component                                                                           (i):(iii):(ii)                                                                      deposits                                                                           metal                                                                              modified                                                                           Al/Me              lot     (iv)     (i)    (iii)   (ii)  mol ratio                                                                           wt % mg   Al   ratio              __________________________________________________________________________    IE 19                                                                             A'  SiO.sub.2 -MAO                                                                         Zr(OPr).sub.4                                                                        indene  AlEt.sub.3                                                                          1:2:4 2    2    MAO  1000               20  B'   "        "     cyclopentadiene                                                                        "     "    1.5  "    "    "                  21  C'  SiO.sub.2                                                                               "      "      AlEt.sub.2 (OEt)                                                                    1:4:8 "    1.8  "    "                  22  D'  Al.sub.2 O.sub.3 -MAO                                                                  Zr(OBu).sub.4                                                                        methylcyclo-                                                                          AlEt.sub.3                                                                          1:2:4 1.8  1.7  "    "                                          pentadiene                                            23  E'  MgCl.sub.2 -Al(OEt).sub.3                                                              Zr(OPr).sub.4                                                                        indene   "     2.0  1.8  "    "                       24  F'  PE polymer-MAO                                                                          "      "       "     "    "    1.9  "    "                  25  G'  SiO.sub.2.Al.sub.2 O.sub.3 -MAO                                                        "      cyclopentadiene                                                                       AlEt.sub.2 Cl                                                                       1:4:10                                                                              "    1.7  "    "                  26  H'  SiO.sub.2 -MAO                                                                         Zr(OEt).sub.4                                                                        bis-cyclo-                                                                            AlEt.sub.3                                                                          1:2:4 "    1.6  "    "                                          pentadienyl-                                                                  dimethyl silane                                       27  I'   "       Zr(OPr).sub.4                                                                        bis-cyclo-                                                                             "     "    1.9  "    "                                               pendadienyl-                                                                  methane                                               28  J'  SiO.sub.2 -AlMe.sub.3                                                                  Zr(OPr).sub.3 Cl                                                                     bis-indenyl-                                                                           "    1:4:8 "    1.8  "    "                                          ethane                                                29  K'  SiO.sub.2 -MAO                                                                         ZrBz.sub.4                                                                           cyclopendadiene                                                                       AlEt.sub.3                                                                          1:3:10                                                                              1.9  1.7  MAO  1000               30  L'   "       TiBz.sub.2                                                                           pentamethyl-                                                                           "     "    2.0  1.9  "    "                                          cyclopoendadiene                                      31  M'   "       HfBz.sub.4 (1)                                                                       cyclopendadiene                                                                        "     "    1.8  2.5  "    "                  32  J'  SiO.sub.2 -AlMe.sub.3                                                                  Zr(OPr).sub.3 Cl                                                                     bis-indenyl-                                                                           "    1:4:8 2.0  1.6  "    "                                          ethane                                                33  J'   "        "     bis-indenyl-                                                                           "     "    2.0  2.7  "    "                                          ethane                                                34  N'  SiO.sub.2 Zr(OPr).sub.4                                                                Zr(OEt).sub.4                                                                        cyclopendadiene                                                                        "    1:2:4 10.0 1.8  "    "                  35  O'  MKg(CO.sub.3).sub.2 -MAO                                                               Zr(OPr).sub.4                                                                        indene   "     "    2.0  1.9  "    "                  CE 4                                                                              T    --      Zr(OPr).sub.4                                                                        indene  AlEt.sub.3                                                                          1:2:4 --   1.7  "    "                  5   U   SiO.sub.2 -MAO                                                                          "      --      "    1:0:4 2    1.6  "    "                  6   V    "        "     indene   "    1:2:0 "    1.5  "    "                  __________________________________________________________________________     IE: Inventive Example                                                         CE: Comparative Example                                                       (1) tetrabenzyl hafnium                                                  

                  TABLE 4                                                         ______________________________________                                                 catalytic         bulk   polymer                                                                             melting                               yield    activity MFR      density                                                                              density                                                                             point                                 g        g/g Me   g/10 min g/cc   g/cm.sup.3                                                                          °C.                            ______________________________________                                        IE 19 76     38,000   0.9    0.38   0.9221                                                                              114.1                               20    98     49,000   3.8    0.40   0.9215                                                                              104.5                               21    57     32,000   4.3    0.41   0.9228                                                                              105.1                               22    73     43,000   2.8    0.39   0.9233                                                                              106.3                               23    67     37,000   0.7    0.30   0.9218                                                                              113.8                               24    76     40,000   0.8    0.33   0.9233                                                                              114.5                               25    86     51,000   3.5    0.40   0.9235                                                                              106.5                               26    61     38,000   2.3    0.41   0.9229                                                                              105.3                               27    44     23,000   4.5    0.38   0.9217                                                                              104.8                               28    95     53,000   0.9    0.40   0.9215                                                                              107.3                               29    73     43,000   6.2    0.36   0.9217                                                                              105.1                               30    66     35,000   1.1    0.35   0.9234                                                                               98.0                               31    72     29,000   2.9    0.39   0.9236                                                                              106.4                               32    97     61,000   1.5    0.42   0.9510                                                                              135.1                               33    99     37,000   1.9    0.37   0.9054                                                                              139.7                               34    94     52,000   8.0    0.37   0.9218                                                                              105.7                               35    47     25,000   0.1    0.31   0.9219                                                                              113.9                               CE 4  95     56,000    0.08  0.20   0.9196                                                                              113.0                               5      0        0     --     --     --    --                                  6     17     11,000   1.3    0.40   0.9280                                                                              115.8                               ______________________________________                                         IE: Inventive Example                                                         CE: Comparative Example                                                  

What is claimed is:
 1. A process for the manufacture of polyolefinswhich comprises homopolymerization or copolymerization of olefinichydrocarbons in the presence of a catalyst composition comprised of afirst component (I) and a second component (II),said first component (I)consisting essentially of a reaction product of:a compound (i) offormula

    Me.sup.1 R.sup.1.sub.n X.sup.1.sub.4-n

wherein R¹ is selected from the group consisting of an alkyl, alkenyl,aryl, alkoxy, aryloxy, and aralkyloxy moiety of 1-24 carbon atoms, X¹ isa halogen atom, Me¹ is zirconium, titanium or hafnium, and n is aninteger of 0≦n≦4; a compound (ii) of formula

    Me.sup.2 R.sup.2.sub.m X.sup.2.sub.z-m

wherein R² is a hydrocarbon group of 1-24 carbon atoms, X² is a halogenatom, Me² is an element of Groups II-III in the Periodic Table, z is thevalence of Me², and m is a number such that 0≦m≦3; a cyclic hydrocarboncompound (iii) having two or more conjugated double bonds; and a carrier(iv) selected from the group consisting of inorganic carriers,particulate polymer carriers, and mixtures thereof, said secondcomponent (II) being a modified organoaluminum compound having Al--O--Albonds derived from the reaction of an organoaluminum compound and water.2. A process as claimed in claim 1 wherein said compound (ii) is anorganoaluminum compound of the formula

    R.sub.3 Al, R.sub.2 AlX, RAlX.sub.2, or R.sub.3 Al.sub.2 X.sub.3

wherein R is a hydrocarbon group of 1-5 carbon atoms and X is a halogenatom.
 3. A process as claimed in claim 1 wherein said cyclic hydrocarboncompound has 2-4 conjugated double bonds and a carbon number of 4-24 inthe molecule.
 4. A process as claimed in claim 1 wherein said inorganiccarrier (iv) is formed of a porous inorganic compound selected from thegroup consisting of a carbonaceous material, metal, metal oxide, metalchloride, metal carbonate, and mixtures thereof, said inorganic carrierhaving a length as measured in the longest dimension of 5-200 μm, asurface area of 50-1,000 m² /g and a pore volume of 0.05-3 cm³ /g.
 5. Aprocess as claimed in claim 1 wherein said particulate polymer carrier(iv) is formed of a thermoplastic or thermosetting resin having anaverage particle size of 5-2,000 μm.
 6. A process as claimed in claim 1wherein R¹ is selected from the group consisting of methyl, ethyl,propyl, butyl, pentyl, hexyl, octyl, vinyl, allyl, phenyl, tolyl, xylyl,methoxy, ethoxy, propoxy, butoxy, pentyloxy, phenoxy, tolyloxy andbenzyloxy.
 7. A process as claimed in claim 1 wherein R² is an alkyl,alkenyl, aryl or aralkyl group.
 8. A process as claimed in claim 1wherein R² is selected from the group consisting of methyl, ethyl,propyl, isopropyl, butyl, pentyl, hexyl, octyl, decyl, dodecyl, vinyl,allyl, phenyl, tolyl, xylyl, benzyl, phenethyl and styryl.
 9. A processas claimed in claim 1 wherein said cyclic hydrocarbon compound (iii) isan aralkylene of 7-24 carbon atoms, cyclopentadiene, substitutedcyclopentadiene, indene, substituted indene, fluorene, substitutedfluorene, cycloheptatriene, substituted cycloheptatriene,cyclooctatetraene, substituted cyclooctatetraene or derivatives thereofcross-linked with an alkylene group wherein said substituted compoundsare substituted with an alkyl or aralkyl group of 1-12 carbon atoms. 10.A process as claimed in claim 9 wherein said alkylene group has 2-8carbon atoms.
 11. A process as claimed in claim 1 wherein said cyclichydrocarbon compound (iii) is selected from the group consisting ofcyclopentadiene, methylcyclopentadiene, ethylcyclopentadiene,t-butylcyclopentadiene, hexylcyclopentadiene, octylcyclopentadiene,1,2-dimethylcyclopentadiene, 1,3-dimethylcyclopentadiene,1,2,4-trimethylcyclopentadiene, 1,2,3,4-tetramethylcyclopentadiene,pentamethylcyclopentadiene, indene, 4-methyl-1-indene,4,7-dimethylindene, 4,5,6,7-tetrahydroindene, fluorene, methylfluorene,cycloheptatriene, methylcycloheptatriene, cyclooctatetraene,methylcyclooctatetraene, bis-indenylethane,bis(4,5,6,7-tetrahydro-1-indenyl)ethane, 1,3-propanedinyl-bis-indene,1,3-propanedinyl-bis(4,5,6,7-tetrahydro)indene, propylene-bis(1-indene),isopropyl(1-indenyl)cyclopentadiene,diphenylmethylene(9-fluorenyl)cyclopentadiene andisopropylcyclopentadienyl-1-fluorene.
 12. A process as claimed in claim1 wherein slurry polymerization or gas-phase polymerization is employed.13. A process as claimed in claim 12 wherein the polymerization reactionis effected under the conditions including a temperature of from 20° C.to 200° C. and pressure of atmospheric to 70 kg/cm² G.
 14. A process asclaimed in claim 1 wherein said first component (I) and the secondcomponent (II) are used in an atomic ratio of aluminum in the secondcomponent (II) to transition metal in the first component (I) of one to100,000.
 15. A process as claimed in claim 1 wherein R¹ is an alkoxy,aryloxy or aralkyloxy moiety of 1-8 carbon atoms.
 16. A process asclaimed in claim 1 wherein the molar ratio of the compound (ii) to thecompound (i) is in the range 0.1:1 to 100:1, and the molar ratio of thecompound (iii) to the compound (i) is in the range 0.1:1 to 100:1.
 17. Aprocess as claimed in claim 1 wherein the molar ratio of the compound(ii) to the compound (i) is in the range 0.1:1 to 100:1, and the molarratio of the compound (iii) to the compound (i) is in the range 0.1:1 to10:1.
 18. A process as claimed in claim 1 wherein the molar ratio of thecompound (ii) to the compound (i) is in the range 1:1 to 100:1, and themolar ratio of the compound (iii) to the compound (i) is in the range1:1 to 10:1.
 19. A process as claimed in claim 1 wherein the ratio ofsaid compound (i) to said carrier (iv) is in the range of 0.01 to 500millimoles of said compound (i) per 100 g of said carrier (iv).
 20. Aprocess as claimed in claim 1 wherein the ratio of said compound (i) tosaid carrier (iv) is in the range of 0.1 to 20 millimoles of saidcompound (i) per 100 g of said carrier (iv).
 21. A process as claimed inclaim 1 wherein the modified organoaluminum compound has 1-100 Al--O--Albonds in the molecule.
 22. A process as claimed in claim 1 wherein themodified organoaluminum compound has 1-50 Al--O--Al bonds in themolecule.
 23. A process as claimed in claim 1 wherein saidorganoaluminum compound of component (II) is a compound of the formula

    R.sub.v.sup.5 AlX.sub.3-v.sup.5

wherein R⁵ is an alkyl, alkenyl, aryl or aralkyl group having a carbonnumber of 1-18, X⁵ is a hydrogen or halogen atom, and 1≦v≦3.
 24. Aprocess as claimed in claim 1 wherein the molar ratio of said modifiedorganoaluminum compound to said water ranges from 0.25:1 to 1.2:1.
 25. Aprocess as claimed in claim 1 wherein the atomic ratio of aluminum inthe second component (II) to the transition metal in the first component(I) is 5:1 to 1,000:1.
 26. A process as claimed in claim 1 wherein thepolymerization reaction is conducted at a temperature of 50°-100° C. anda pressure of atmospheric pressure to 20 kg/cm² G.
 27. A process asclaimed in claim 1 wherein the polymerization is a homo-polymerizationof α-olefins having a carbon number of 2-12.
 28. A process as claimed inclaim 27 wherein said α-olefin is ethylene.
 29. A process as claimed inclaim 1 wherein the polymerization is a co-polymerization of ethyleneand α-olefins having a carbon number of 3-12.
 30. A process as claimedin claim 29 wherein said α-olefin is used in an amount of less than 40mol % of total monomers.
 31. A process as claimed in claim 1 whereinsaid n is an integer of 0<n<4.